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Rhenium recovery

a technology applied in the field of rhenium and rhenium compounds, can solve the problems of large quantities of hydrogen gas generation, and achieve the effect of reducing the risk of explosion

Active Publication Date: 2015-02-17
MARITIME HOUSE METALS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

With respect the direct acid attack of rhenium (Re) superalloy, a major problem with hydrochloric acid and sulfuric acid leaching processes is the generation of large quantities of hydrogen gas, in the reaction of the nickel and cobalt values with the acid.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0043]A super-alloy sample, in finely divided form of particle size up to about 100 microns, was assayed and found to have the following metal composition:

Rhenium 2.85%;

Nickel 53.6%;

Cobalt 9.9%;

Molybdenum 2.0%;

Aluminum 4.2%; and

Chromium 3.1%;

with the balance of the composition comprising Titanium (Ti), Tungsten (W) and Tantalum (Ta).

[0044]The finely divided material was added slowly to an agitated leach vessel containing acid solution, to a solids content of 100 kg / m3 of solution. Five experiments were run, each at a temperature of about 70° C. to about 80° C. and over duration of about 4 to about 6 hours. In each experiment, the acid solution was hydrochloric acid, but also containing different amounts of nitric acid. The percentage of dissolved nickel and of dissolved rhenium was measured at the end of each experiment. The nitric acid contents, expressed as cubic meters per ton of feed (m3 / T), and analytical results are given in Table 1 below.

[0045]

TABLE 1Nitric (70%Concentration)...

example 2

[0047]Another series of similar experiments was conducted, using different starting materials. Each experiment used a leach time of about 5 hours, a temperature of about 70° C. to about 90° C., and a leach acid solution of about 1.8 to about 3.0 cubic meters of nitric acid per ton of feed. Feed type A was a nickel based super-alloy of North American origin. Feed type B was sludge from a molybdenite roasting of North American origin. Feed type C was sludge from a molybdenite roasting of European origin. Feed type D was a super-alloy from Europe. The feed types where assayed for the percent (%) composition of rhenium (Re), nickel (Ni), molybdenite (Mo) and cobalt (Co). The results of the percent compositional analysis of the feed types used are provided below in Table 2, and the results of the leach in Table 3. As feed types A and D were super-alloys, the balance of the composition for feed types A and D is comprised of tantalum (Ta), tungsten (W), and titanium (Ti). Feed types B and ...

example 3

[0050]A sample of Re-containing super-alloy from turbine blades was also subjected to the process in an experiment. The sample subjected to the process in this example was provided as a single, larger piece of material having a size of approximately 3 cm by approximately 10 cm with an average thickness or cross-sectional dimension of about 1.3 cm. The sample was assayed for percent composition and it was found to comprise 2.85% Re, 53.6% Ni, 9.9% Co, 3.1% Cr, 4.2% Al, and 2% Mo with the balance of the composition comprised of Ta, W and Ti.

[0051]The sample was subjected the leaching process, as described above, in a solution comprising hydrochloric and nitric acids (respectively 37% and 70% solutions by weight). The volume ratio of the acids was 3 (HCl) to 1 (NO3) (3:1) and was provided in a volume of 10 liters per kilogram of the super-alloy blade sample (L / kg). The supernatant solution was agitated and kept at a temperature of about 80° C. The results of the amount of Re and Ni ext...

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PUM

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Abstract

There is provided a hydrometallurgical process of recovering rhenium values from mixtures thereof with other metal values in which the rhenium values constitute a minority amount, for example super-alloys, which comprises subjecting the mixture to strongly oxidizing acid conditions, preferably an aqueous mixture of hydrochloric acid and nitric acid, so as to form perrhenate species of at least the major proportion of the rhenium values in the mixture, dissolving the perrhenate species and other soluble metal species in aqueous solution, removing insoluble metal species from the aqueous solution, and isolating the rhenium species from the solution.

Description

RELATED APPLICATION[0001]The present application is a U.S. nationalization under 35 U.S.C. §371 of International Application No. PCT / CA2010 / 000333, filed Mar. 11, 2010, which claims benefit of priority to U.S. Provisional Patent Application No. 61 / 159,883, filed Mar. 13, 2009, entitled “RHENIUM RECOVERY”. The disclosures set forth in the referenced patent applications are incorporated herein by reference in their entireties, including all information as originally submitted to the U.S. Patent and Trademark Office.FIELD OF THE DISCLOSURE[0002]This disclosure relates to rhenium and rhenium compounds. More specifically, it relates to processes for extracting rhenium and rhenium compounds from compositions containing rhenium and rhenium compounds along with other metals and metal compounds, for example alloys, super-alloys, ores and metallurgical residues.BACKGROUND OF THE DISCLOSURE[0003]Rhenium (Re) is a rare, greyish-white, heavy, poly-valent transition metal, of atomic number 75 and...

Claims

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Application Information

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Patent Type & Authority Patents(United States)
IPC IPC(8): C01G45/00C22B47/00C01G47/00C22B3/06C22B3/10C22B3/42C22B3/44C22B7/00C22B11/02C22B61/00
CPCC22B61/00C22B3/065C22B3/10C22B3/42C22B3/44C22B7/007C01G47/00C22B11/021Y02P10/20
Inventor FERRON, CESARE G.SEELEY, LARRY E.
Owner MARITIME HOUSE METALS
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